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Isothermal Vapor-Liquid Equilibria in the Two Binary and the Ternary Systems Composed of tert-Amyl Methyl Ether, tert-Butanol, and Isooctane
- 1.0359249 - ÚCHP 2012 RIV US eng J - Journal Article
Bernatová, Svatoslava - Pavlíček, Jan - Wichterle, Ivan
Isothermal Vapor-Liquid Equilibria in the Two Binary and the Ternary Systems Composed of tert-Amyl Methyl Ether, tert-Butanol, and Isooctane.
Journal of Chemical and Engineering Data. Roč. 56, č. 4 (2011), s. 783-788. ISSN 0021-9568. E-ISSN 1520-5134
R&D Projects: GA ČR GA104/07/0444
Institutional research plan: CEZ:AV0Z40720504
Keywords : vapor-liquid equilibrium * experimental data * prediction
Subject RIV: CF - Physical ; Theoretical Chemistry
Impact factor: 1.693, year: 2011
Vapor–liquid equilibrium data in the two binary methyl 2-methyl-2-butyl ether (tert-amyl methyl ether, TAME) + 2-methyl-2-propanol (tert-butanol), TAME + 2,2,4-trimethylpentane (isooctane) systems, and in the ternary TAME + tert-butanol + isooctane system are reported. The data were measured isothermally at 318.13, 328.20 and 338.28 K covering the pressure range 15–51 kPa. The binary vapor–liquid equilibrium data were correlated using the Wilson and NRTL equations by means of a new algorithm; resulting parameters were then used for calculation of phase behavior in the ternary system and for subsequent comparison with experimental data.
Permanent Link: http://hdl.handle.net/11104/0197067
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